The invention belongs to the technical field of heat exchangers. The invention relates more specifically to plate heat exchangers filled with a powder designed to initiate a physical/chemical reaction.
Brazed-plate heat exchangers are traditionally used in the cryogenic industry for gas separation and liquefaction, in the energy and petrochemical sectors.
As part of an energy transition with major CO2 emission reduction targets, many countries are showing increasing interest in new energy sources. In this context, brazed-plate heat exchangers are being adapted to new industrial-scale processes. This is the case for hydrogen liquefaction processes linked to the development of hydrogen mobility.
Hydrogen, for example, is more stable at low temperatures in the para hydrogen state than in the ortho hydrogen state. At low temperatures, particularly liquefaction temperatures, ortho hydrogen tends to spontaneously transform into para hydrogen, releasing unwanted heat.
To keep hydrogen in its liquid state, there are two options. A first option is to continuously extract the heat released by the conversion of ortho hydrogen into para hydrogen. In practice, this technique proves to be particularly energy-intensive, and uneconomical on an industrial scale.
A second option is to eliminate ortho hydrogen by converting it to para hydrogen. An exothermic catalytic reaction combined with cooling converts most of the ortho hydrogen into para hydrogen. Spontaneous conversions of ortho hydrogen to para hydrogen are then reduced.
This second option is one of the areas wherein the present invention can be applied.
Due to the use of a catalyst, often in powder form, inserted into the heat exchanger after the brazing operations, it is necessary to use hydrogen dispensing heads with large openings whose cross-section is substantially equal to that of said heat exchanger. This ensures even powder distribution in the exchanger compartments.
This means that the dispensing heads are particularly large, which has an impact on the heat exchanger.
Conventional heat exchangers typically comprise longitudinal and end bars defining compartments separated from each other by hermetic separating walls.
In the case of distributor heads whose cross-section is roughly equal to the cross-section of the heat exchanger, there are no end bars in catalyst-containing compartments, as they would impede the insertion of catalyst in powder form. However, the overall structure of the heat exchanger is weakened, as the end bars contribute to the mechanical strength of the heat exchanger and to the distribution of welding stresses.
During the assembly operation, the dispensing heads are welded to said heat exchanger. Weld cooling, material expansion, and material contraction cause mechanical stresses that can deform the main structure of the heat exchanger, reducing its efficiency. A further disadvantage is that these deformations make it more difficult to fill the heat exchanger with powdered catalyst, leading to maldistribution of the catalyst, which is detrimental to the unit's performance.
The invention aims to address these drawbacks.
For this purpose, a heat exchanger comprising:
Such a heat exchanger enables the exchanger structure to absorb the mechanical stresses inherent in cooling the weld. This makes it easier to fill with powder.
Various additional features can be provided alone or in combination:
Further features and advantages of the invention will become apparent from the following detailed description, which can be understood with reference to the accompanying drawings, wherein:
The heat exchanger 1 comprises several longitudinal bars 2 together defining a body 3 provided with compartments 4 wherein a fluid is able to circulate. Each compartment 4 is bordered laterally along the Y axis by a longitudinal bar 2. The compartments 4 are adjacent to each other. In other words, compartments 4 are juxtaposed one on top of the other.
The heat exchanger 1 comprises separating walls 5. A separating wall 5 is located between each compartment 4. Thus, a separating wall 5 separates the compartments 4 from each other along the Z axis.
On either side of the heat exchanger 1 along the Z axis, the heat exchanger comprises an end compartment 6 located at the transverse ends 7. A closing wall 8 is arranged on each end compartment 6, thus closing the heat exchanger 1.
As shown in
The fluid thus distributed by the dispensing head 9 is distributed into the accessible compartments 4 arranged along the Z axis.
The heat exchanger 1 further comprises a collection head, not shown in the drawings, arranged opposite the dispensing head 9. The collection head collects the fluid leaving the compartments.
With reference to
The compartments 11 are sealed off so as to prevent, at least in part, the circulation of fluid in them. Advantageously, a sealed-off compartment 11 is sealed by means of a transverse closure bar 12, 13 extending along the Y axis.
The dispensing head 9 is attached to the body 3 by welding. When the welding is complete, the cooling of a metal 15 causes mechanical stresses on the body 3. These mechanical stresses are commonly referred to as “material shrinkage”.
Advantageously, at least one of the sealed-off compartments 11 is, at least in part, deformable. The deformable 11 compartment thus absorbs the mechanical stress caused by the welding operation. The structure of heat exchanger 1 is not damaged. In the following, reference is made to the deformable sealed-off compartment 11, for each adjacent compartment 16.
Advantageously, the heat exchanger 1 comprises an end closure bar 13, extending along the Y axis and arranged inside the end compartment 6. The end closure bar 13 is arranged at the inlet 17 of the end compartment 6. The end closure bar 13 thus blocks fluid entry into the end compartment 6.
Advantageously, the end closure bar 13 is beveled on its part facing the dispensing head 9. The end closure bar 13 thus defines an orifice 14 with the dispensing head 9. The orifice 14 is delimited laterally by the dispensing head 9 on one side and by the end closure bar 13 on the other. The weld is made in the orifice 14. In other words, the weld metal 15 is deposited in the orifice 14.
The end closure bar 13, in addition to acting as a support for the weld metal 15, prevents significant deformation of the end compartment 6. Indeed, deformation of the end compartment 6 would tend to weaken the dispensing head 9 or the collection head.
Advantageously, the body 3 comprises an adjacent compartment 16 which is at least partially deformable. The compartment 16 is enclosed and adjacent to the end compartment 6. As can be seen in
Advantageously, the adjacent compartment 16 comprises a closure bar 12 designed to block the passage of fluid.
The body 3 of the heat exchanger 1 comprises a deformable zone 18. The deformable zone 18 of the adjacent compartment 16 is the part of said adjacent compartment 16 that deforms under the effect of the stresses generated by the welding operation.
The deformable zone 18, thus localized, maintains the integrity of the heat exchanger 1 following material shrinkage.
The deformable zone 18 extends from the inlet 17 over a distance d measured along the X axis. Advantageously, the distance d is at least 3 centimeters.
Advantageously, the body 3 of the heat exchanger 1 comprises a reinforcement compartment 19. The reinforcement compartment 19 is located adjacent to the deformable compartment 16. The reinforcement compartment 19 is open, so fluid can flow through it. The reinforcement compartment 19 stops the deformation of the deformable zone 18 in order to prevent the cross-section of other open compartments 10 from being reduced. At the end of the welding operation, the reinforcement compartment 19 does not deform significantly.
Advantageously, the body 3 comprises wave plates 20. The wave plates 20 define circulation channels wherein the fluid can flow. The wave plates 20 are arranged in the open compartments 10 and in the closed compartments 11.
In the open compartments 10, the wave plates 20 guide the fluid through the channels. In the case of the catalytic heat exchangers 1, the channels are filled with a catalytic agent, usually in powder form. The fluid passes through the channels, and therefore through the powder acting as a catalyst.
In the closed compartments 11, the wave plates 20 act as a “deformable damper”. In this way, they impart a certain resistance to stress to these sealed compartments 11 to prevent them from deforming too easily during various operations such as brazing or welding.
Advantageously, deformable wave plates 30 defining fluid circulation channels are arranged in the deformable zone 18 of the deformable compartment 16. Reinforcement wave plates 40, defining fluid circulation channels, are arranged in a reinforced zone 22 of the reinforcement compartment 19. The wave plates 30 in the deformable compartment 16 have a lower critical buckling load than the reinforcement wave plates 40. This makes it possible to locate the deformable zone 18. Thus, it is the deformable zone 18 that will deform after the welding operation, while the reinforced zone 22 will not deform significantly. In this way, the deformation can be controlled by focusing it on a desired point deemed to be safe for the heat exchanger. The deformation is not random. By deformation, we mean that the deformable zone 18 deforms elastically and is held in an elastically deformed position by the weld 15. The deformation is therefore not ductile and irreversible.
Advantageously, the reinforced zone 22 extends over a distance r measured along the X axis from the inlet 17. The distance r is at least 3 centimeters. A reinforced zone 22 with these dimensions strengthens the heat exchanger and prevents deformation of other open compartments 10 located below the reinforcement compartment 19.
Number | Date | Country | Kind |
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FR2114689 | Dec 2021 | FR | national |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2022/085326 | 12/12/2022 | WO |